US11224845B2 - System, method, and apparatus to oxygenate water - Google Patents

System, method, and apparatus to oxygenate water Download PDF

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US11224845B2
US11224845B2 US17/247,578 US202017247578A US11224845B2 US 11224845 B2 US11224845 B2 US 11224845B2 US 202017247578 A US202017247578 A US 202017247578A US 11224845 B2 US11224845 B2 US 11224845B2
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water
mixing chamber
oxygenator
air inlet
baffles
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Terry M. White
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3131—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • B01F5/0451—
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/74—Treatment of water, waste water, or sewage by oxidation with air
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B01F23/23231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
    • B01F23/232312—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit the guiding constructions being baffles for guiding the flow up-and-down or from left-to-right
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23761—Aerating, i.e. introducing oxygen containing gas in liquids
    • B01F23/237611—Air
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4316—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being flat pieces of material, e.g. intermeshing, fixed to the wall or fixed on a central rod
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • B01F25/4336—Mixers with a diverging cross-section
    • B01F3/04524—
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F7/00—Aeration of stretches of water
    • B01F2003/04879—
    • B01F2005/0005—
    • B01F2005/0025—
    • B01F2005/004—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F2025/91—Direction of flow or arrangement of feed and discharge openings
    • B01F2025/911—Axial flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F2025/91—Direction of flow or arrangement of feed and discharge openings
    • B01F2025/916—Turbulent flow, i.e. every point of the flow moves in a random direction and intermixes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F2025/91—Direction of flow or arrangement of feed and discharge openings
    • B01F2025/919—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings
    • B01F2025/9191—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings characterised by the arrangement of the feed openings for one or more flows, e.g. for the mainflow and the flow of an additional component
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/305—Treatment of water, waste water or sewage
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/35—Mixing inks or toners
    • B01F2215/0052—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23761—Aerating, i.e. introducing oxygen containing gas in liquids
    • B01F23/237612—Oxygen

Definitions

  • the present invention relates to water oxygenation, and more particularly to oxygenation of water sources in a retention reservoir for discharge to a waterway.
  • Water retention reservoirs are employed for many industrial processes to contain water used in the industrial process for subsequent treatment before the contained water is discharged into a waterway. Oxygenation of the contained water is a common treatment that is required for protection of the environment.
  • Discharge of improperly oxygenated water into a waterway is deleterious to the environment.
  • States and other jurisdictions may specify a minimum oxygen content for water discharged into a waterway within the jurisdiction. Failure to meet a specified oxygen content can result in significant fines and interruption of plant operation.
  • oxygenation technologies include mechanical drivers, agitators, fountains, and bottom diffusion aerators. These oxygenation technologies can be expensive and often require extended temporal periods to properly elevate the dissolved oxygen level to a level that is suitable for discharge into a waterway.
  • a water oxygenator in one aspect of the present invention, includes an elongate cylindrical tube having a first end, a second end, an outer sidewall defining a main mixing chamber within an interior cavity of the elongate cylindrical tube.
  • a plurality of baffles is disposed in a spaced apart relation along a longitudinal length of the main mixing chamber.
  • a water inlet is provided at the first end. The water inlet is adapted to be coupled to a source of water contained in a retention reservoir. The water inlet has a diameter less than a diameter of the elongate cylindrical tube.
  • a water outlet is provided at the second end and has a diameter less than diameter of the elongate cylindrical tube.
  • a first frusto-conical sidewall connects the water inlet with the outer sidewall.
  • the frusto-conical sidewall defines an initial mixing chamber.
  • An air inlet tube protrudes through the first frusto-conical sidewall into the initial mixing chamber.
  • the air inlet tube is adapted to be coupled to a high-volume, low-pressure air source.
  • each of the plurality of baffles further include a rectangular plate.
  • An arcuate edge surface is defined along first opposed ends of the rectangular plate.
  • a generally linear side edge is defined along second opposed ends of the plate.
  • Each of the plurality of baffles are attached to an interior sidewall of the elongate cylindrical tube at the arcuate edge surface.
  • Each of the plurality of baffles may be radially offset from each other along a longitudinal length of the main mixing chamber.
  • the air inlet tube further includes an injector defined at a distal end of the air inlet tube.
  • the injector is oriented to project in a downstream direction along a longitudinal centerline of the initial mixing chamber.
  • An upstream side of the injector and the air inlet tube are oriented to obstruct a water flow from the source of water to introduce a turbulent zone at an exit of the injector within the initial mixing chamber.
  • a second frusto-conical sidewall connects the outer sidewall with the water outlet.
  • a system for oxygenating a source of water held within a containment reservoir includes a water oxygenator formed as an elongate cylindrical tube having a first end, a second end, an outer sidewall defining a main mixing chamber within an interior cavity.
  • a water inlet is provided at the first end.
  • a fluid outlet is provided at the second end and configured to discharge a flow of oxygenated water from the water oxygenator.
  • a plurality of baffles is contained within the interior cavity and are disposed in a spaced apart radially offset relation along a longitudinal length of the elongate cylindrical tube.
  • a first frusto-conical sidewall connects the water inlet with the elongate cylindrical tube and defines an initial mixing chamber therein.
  • An air inlet tube projects through the first frusto-conical sidewall into the initial mixing chamber.
  • a water pump configured to communicate the source of water from the containment reservoir to the water inlet.
  • An air source is configured to deliver high volume, low pressure air flow to the air inlet tube.
  • each of the plurality of baffles include a rectangular plate.
  • An arcuate edge surface is defined along first opposed ends of the rectangular plate.
  • a generally linear side edge is defined along second opposed ends of the rectangular plate.
  • each of the plurality of baffles are attached to an interior sidewall of the elongate cylindrical tube at the arcuate edge surface.
  • An injector is defined at a distal end of the air inlet tube. The injector is oriented to project in a downstream direction along a longitudinal centerline of the initial mixing chamber.
  • an upstream side of the injector and the air inlet tube are oriented to obstruct a water flow from the source of water to introduce a turbulent zone at an exit of the injector within the initial mixing chamber.
  • a second frusto-conical sidewall connects the outer sidewall with the fluid outlet.
  • FIG. 1 is a front perspective view of a water oxygenator.
  • FIG. 2 is a partial cutaway view of the water oxygenator taken along lines 2 - 2 of FIG. 1 .
  • FIG. 3 is a detail cross sectional view of an inlet end of the water oxygenator taken along line 3 - 3 of FIG. 1 .
  • FIG. 4 is a schematic view of a water oxygenation system.
  • FIG. 5 is a flowchart of a water oxygenation process.
  • a water oxygenator 10 of a water oxygenation system is illustrated.
  • the water oxygenator 10 shown is a water-driven device, in the sense that its operation is only dependent on a flow of water through 100 the water oxygenator 10 and a flow of an oxygen containing gas 120 through an inlet 40 into the water oxygenator 10 .
  • the water oxygenator 10 is formed as an elongate cylindrical tube having a water inlet 30 at a first end, a water outlet 50 at a second end, and an air inlet tube 40 proximal to the first end.
  • the elongate cylindrical tube has an outer sidewall 20 defining a mixing chamber 60 within an interior cavity of the water oxygenator 10 .
  • the mixing chamber 60 includes a plurality of baffles 70 that are disposed in a spaced apart relation along a longitudinal length of the interior cavity.
  • Each of the water inlet 30 and the water outlet 50 may include a frusto-conical tapered sidewall 22 connecting to the outer sidewall 20 of the water oxygenator.
  • the tapered sidewall 22 is formed by diverging sidewalls from the water inlet 40 to the outer sidewall 20 .
  • the tapered sidewall 24 is formed by converging sidewalls between the outer sidewall 20 and the water outlet 50 .
  • Attached proximal to the water inlet 30 is a smaller air inlet tube 40 that provides an inlet portal for a high-volume, low-pressure air source (generally provided by a turbine 120 ).
  • This air-inlet 40 connects to an initial mixing chamber 62 in communication with the mixing chamber 60 of the interior cavity of the water oxygenator 10 .
  • the air inlet tube 40 protrudes through the frusto-conical sidewall 62 and extends into a longitudinal centerline of the initial mixing chamber 62 , terminating in an injector 42 at a distal end of the air inlet tube 40 .
  • the injector 42 is dimensioned to open towards the mixing chamber 60 with a downstream orientation.
  • the injector 42 is angled generally perpendicular to a water flow 80 carried through the water inlet 30 .
  • An upstream side of the injector 42 and the air inlet tube 40 are oriented to obstruct the incoming water flow 80 to introduce a turbulent zone at the exit of the injector 42 into the interior cavity.
  • Each of the plurality of baffles 70 are formed as a generally rectangular plate having arcuate ends 72 to mate and join with an interior sidewall of the mixing chamber 60 . Fluid flow through the mixing chamber 60 is provided between a side edge 74 of each of the plurality of baffles 70 offset from the arcuate ends and the interior sidewall of the mixing chamber 60 .
  • the arcuate ends 72 of the baffles 70 may be welded to the mixing chamber 60 .
  • the orientation of each of the plurality of baffles 70 are disposed in a radially offset relationship, preferably at 90 degree angles, leaving a space between each side edge 74 and the interior sidewall of the mixing chamber 60 .
  • Operation of the water oxygenator 10 may be seen in reference to FIGS. 3 and 4 , which harnesses the power of a water flow 80 through the water oxygenator 10 to mix with and to extract oxygen present in the air source 90 .
  • the water flow 80 and the air flow 90 mix in a plurality of turbulence zones defined throughout the water oxygenator 10 .
  • An initial turbulence zone is present at the juncture of the water 80 and the air flow 90 from the water inlet tube 40 , and each of the plurality of baffles 70 within the mixing chamber 60 .
  • the plurality of turbulence zones increases the dissolved oxygen content of the water flow 80 for discharge in an environmentally compliant condition.
  • a process of oxygenating a water source retained in a containment reservoir according to other aspects of the present is shown in reference to FIG. 5 and includes the following:
  • the basic structure of the water oxygenator 10 may remain the same but the water oxygenator 10 may be made of alternative materials, such as aluminum or steel, depending on the intended application and flow volumes.
  • Advantages of the system include: 1. Low construction cost; 2. Ease of use; 3. Scalability; 4. Low energy consumption; 5. Minimal moving parts; 6. Simplicity (only water and air required); 7. Wide application; and 8. High output.
  • the system may include a water containment reservoir 200 , containing a volume of water 100 having a lowered oxygen content.
  • a water pump 110 communicates the water 100 from the containment reservoir 200 to the water inlet 30 of the water oxygenator 10 .
  • a low pressure, high volume air source 120 which may be provided by a turbine or the like, supplies air 90 to the air inlet tube 40 of the water oxygenator 10 . After passage through the water oxygenator 10 , high oxygen content water is discharged from the outlet 50 in an environmentally compliant condition.
  • the water oxygenator and oxygenation system is effective in significantly elevating the dissolved oxygen content of the water in the retention reservoir for discharge into a waterway.
  • the foregoing results were obtained with a water oxygenator 10 having a water inlet 30 of 3 inches, a diameter of 5 inches along the sidewall 60 , and a water outlet diameter of 3 inches.
  • the water flow 80 through the water oxygenator was maintained at a nominal flow of 100 gallons per minute.
  • the air flow 90 through the water oxygenator 10 was maintained at a nominal flow of 50 SCFM at a pressure of 4 psi.

Abstract

A system, method, and apparatus for oxygenation of a source of water, to increase the dissolved oxygen content of water. Aspects of the present invention harnesses and directs the power of water flowing through the system to extract oxygen present in air, rather than relying on the injection of gas or using other mechanical means. The water oxygenator is formed as an elongate cylindrical tube having a water inlet at a first end, a water outlet at a second end, and an air inlet proximal to the first end. The elongate cylindrical tube has an outer sidewall defining a mixing chamber within an interior cavity of the water oxygenator. The mixing chamber includes a plurality of baffles that are disposed in a spaced apart relation along a longitudinal length of the interior cavity.

Description

CROSS-REFERENCE TO RELATED APPLICATION
This application claims the benefit of priority of U.S. provisional application No. 62/965,335, filed Jan. 24, 2020, the contents of which are herein incorporated by reference.
BACKGROUND OF THE INVENTION
The present invention relates to water oxygenation, and more particularly to oxygenation of water sources in a retention reservoir for discharge to a waterway.
Water retention reservoirs are employed for many industrial processes to contain water used in the industrial process for subsequent treatment before the contained water is discharged into a waterway. Oxygenation of the contained water is a common treatment that is required for protection of the environment.
Discharge of improperly oxygenated water into a waterway is deleterious to the environment. States and other jurisdictions may specify a minimum oxygen content for water discharged into a waterway within the jurisdiction. Failure to meet a specified oxygen content can result in significant fines and interruption of plant operation.
Currently available oxygenation technologies include mechanical drivers, agitators, fountains, and bottom diffusion aerators. These oxygenation technologies can be expensive and often require extended temporal periods to properly elevate the dissolved oxygen level to a level that is suitable for discharge into a waterway.
As can be seen, there is a need for an improved system, method, and apparatus for oxygenating water of a retention reservoir for discharge into a waterway at high volumes.
SUMMARY OF THE INVENTION
In one aspect of the present invention, a water oxygenator is disclosed. The water oxygenator includes an elongate cylindrical tube having a first end, a second end, an outer sidewall defining a main mixing chamber within an interior cavity of the elongate cylindrical tube. A plurality of baffles is disposed in a spaced apart relation along a longitudinal length of the main mixing chamber. A water inlet is provided at the first end. The water inlet is adapted to be coupled to a source of water contained in a retention reservoir. The water inlet has a diameter less than a diameter of the elongate cylindrical tube. A water outlet is provided at the second end and has a diameter less than diameter of the elongate cylindrical tube. A first frusto-conical sidewall connects the water inlet with the outer sidewall. The frusto-conical sidewall defines an initial mixing chamber. An air inlet tube protrudes through the first frusto-conical sidewall into the initial mixing chamber. The air inlet tube is adapted to be coupled to a high-volume, low-pressure air source.
In some embodiments, each of the plurality of baffles further include a rectangular plate. An arcuate edge surface is defined along first opposed ends of the rectangular plate. A generally linear side edge is defined along second opposed ends of the plate. Each of the plurality of baffles are attached to an interior sidewall of the elongate cylindrical tube at the arcuate edge surface. Each of the plurality of baffles may be radially offset from each other along a longitudinal length of the main mixing chamber.
In some embodiments, the air inlet tube further includes an injector defined at a distal end of the air inlet tube. The injector is oriented to project in a downstream direction along a longitudinal centerline of the initial mixing chamber. An upstream side of the injector and the air inlet tube are oriented to obstruct a water flow from the source of water to introduce a turbulent zone at an exit of the injector within the initial mixing chamber.
In other embodiments, a second frusto-conical sidewall connects the outer sidewall with the water outlet.
In another aspect of the invention, a system for oxygenating a source of water held within a containment reservoir is disclosed. The system includes a water oxygenator formed as an elongate cylindrical tube having a first end, a second end, an outer sidewall defining a main mixing chamber within an interior cavity. A water inlet is provided at the first end. A fluid outlet is provided at the second end and configured to discharge a flow of oxygenated water from the water oxygenator. A plurality of baffles is contained within the interior cavity and are disposed in a spaced apart radially offset relation along a longitudinal length of the elongate cylindrical tube. A first frusto-conical sidewall connects the water inlet with the elongate cylindrical tube and defines an initial mixing chamber therein. An air inlet tube projects through the first frusto-conical sidewall into the initial mixing chamber. A water pump configured to communicate the source of water from the containment reservoir to the water inlet. An air source is configured to deliver high volume, low pressure air flow to the air inlet tube.
In some embodiments, each of the plurality of baffles include a rectangular plate. An arcuate edge surface is defined along first opposed ends of the rectangular plate. A generally linear side edge is defined along second opposed ends of the rectangular plate.
In some embodiments, each of the plurality of baffles are attached to an interior sidewall of the elongate cylindrical tube at the arcuate edge surface. An injector is defined at a distal end of the air inlet tube. The injector is oriented to project in a downstream direction along a longitudinal centerline of the initial mixing chamber.
In other embodiments, an upstream side of the injector and the air inlet tube are oriented to obstruct a water flow from the source of water to introduce a turbulent zone at an exit of the injector within the initial mixing chamber.
In other embodiments, a second frusto-conical sidewall connects the outer sidewall with the fluid outlet.
These and other features, aspects and advantages of the present invention will become better understood with reference to the following drawings, description and claims.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a front perspective view of a water oxygenator.
FIG. 2 is a partial cutaway view of the water oxygenator taken along lines 2-2 of FIG. 1.
FIG. 3 is a detail cross sectional view of an inlet end of the water oxygenator taken along line 3-3 of FIG. 1.
FIG. 4 is a schematic view of a water oxygenation system.
FIG. 5 is a flowchart of a water oxygenation process.
 DETAILED DESCRIPTION
The following detailed description is of the best currently contemplated modes of carrying out exemplary embodiments of the invention. The description is not to be taken in a limiting sense but is made merely for the purpose of illustrating the general principles of the invention.
As seen in reference to the drawings of FIGS. 1-3, a water oxygenator 10 of a water oxygenation system is illustrated. The water oxygenator 10, shown is a water-driven device, in the sense that its operation is only dependent on a flow of water through 100 the water oxygenator 10 and a flow of an oxygen containing gas 120 through an inlet 40 into the water oxygenator 10.
The water oxygenator 10 is formed as an elongate cylindrical tube having a water inlet 30 at a first end, a water outlet 50 at a second end, and an air inlet tube 40 proximal to the first end. The elongate cylindrical tube has an outer sidewall 20 defining a mixing chamber 60 within an interior cavity of the water oxygenator 10. The mixing chamber 60 includes a plurality of baffles 70 that are disposed in a spaced apart relation along a longitudinal length of the interior cavity.
Each of the water inlet 30 and the water outlet 50 may include a frusto-conical tapered sidewall 22 connecting to the outer sidewall 20 of the water oxygenator. In the case of the water inlet 40, the tapered sidewall 22 is formed by diverging sidewalls from the water inlet 40 to the outer sidewall 20. In the case of the water outlet 50, the tapered sidewall 24 is formed by converging sidewalls between the outer sidewall 20 and the water outlet 50.
Attached proximal to the water inlet 30 is a smaller air inlet tube 40 that provides an inlet portal for a high-volume, low-pressure air source (generally provided by a turbine 120). This air-inlet 40 connects to an initial mixing chamber 62 in communication with the mixing chamber 60 of the interior cavity of the water oxygenator 10. The air inlet tube 40 protrudes through the frusto-conical sidewall 62 and extends into a longitudinal centerline of the initial mixing chamber 62, terminating in an injector 42 at a distal end of the air inlet tube 40. The injector 42 is dimensioned to open towards the mixing chamber 60 with a downstream orientation. The injector 42 is angled generally perpendicular to a water flow 80 carried through the water inlet 30. An upstream side of the injector 42 and the air inlet tube 40 are oriented to obstruct the incoming water flow 80 to introduce a turbulent zone at the exit of the injector 42 into the interior cavity.
Each of the plurality of baffles 70 are formed as a generally rectangular plate having arcuate ends 72 to mate and join with an interior sidewall of the mixing chamber 60. Fluid flow through the mixing chamber 60 is provided between a side edge 74 of each of the plurality of baffles 70 offset from the arcuate ends and the interior sidewall of the mixing chamber 60. In the case of a metallic structure, the arcuate ends 72 of the baffles 70 may be welded to the mixing chamber 60. The orientation of each of the plurality of baffles 70 are disposed in a radially offset relationship, preferably at 90 degree angles, leaving a space between each side edge 74 and the interior sidewall of the mixing chamber 60.
Operation of the water oxygenator 10 may be seen in reference to FIGS. 3 and 4, which harnesses the power of a water flow 80 through the water oxygenator 10 to mix with and to extract oxygen present in the air source 90. The water flow 80 and the air flow 90 mix in a plurality of turbulence zones defined throughout the water oxygenator 10. An initial turbulence zone is present at the juncture of the water 80 and the air flow 90 from the water inlet tube 40, and each of the plurality of baffles 70 within the mixing chamber 60. The plurality of turbulence zones increases the dissolved oxygen content of the water flow 80 for discharge in an environmentally compliant condition.
A process of oxygenating a water source retained in a containment reservoir according to other aspects of the present is shown in reference to FIG. 5 and includes the following:
    • 1) Water 100 from a containment reservoir is delivered via a pump 110 to enters the water inlet 30 of the water oxygenator 10 through the water inlet 30.
    • 2) An air source 120, such as a turbine, generates a steady, high volume of the air flow 90 at a low pressure, is operatively connected to enter through the air inlet tube 40.
    • 3) The water 80 and air 90 come together in the first mixing chamber 62, creating the initial turbulence zone. As the water 80 flows into the elongate tube of the mixing chamber 60 it begins to mix with oxygen carried in the air source 90.
    • 4) The force of the water flow 80 at a point of impact with each of the plurality of baffles 70 generates a pressure and additional turbulence which forces the water 80 to flow around the side edges 74 of the baffle 70. Turbulence at the back side of the baffle 70 creates a low-pressure void for oxygenation of the water.
The above-described process is repeated with each additional baffle 70. With the angular offset between a preceding and a subsequent baffle 70, turbulent flow is induced, with associated changes in pressure as the water 80 and air 90 flow through the water oxygenator 10 and around the offset baffles 70 which results in a thorough mixing of the air 90 and the water 80, resulting in an immediate and significant increase in the dissolved oxygen content of the water discharged from the outlet 50.
The basic structure of the water oxygenator 10 may remain the same but the water oxygenator 10 may be made of alternative materials, such as aluminum or steel, depending on the intended application and flow volumes. Advantages of the system include: 1. Low construction cost; 2. Ease of use; 3. Scalability; 4. Low energy consumption; 5. Minimal moving parts; 6. Simplicity (only water and air required); 7. Wide application; and 8. High output.
The system according to aspects of the present invention is illustrated in reference to FIG. 4. The system may include a water containment reservoir 200, containing a volume of water 100 having a lowered oxygen content. A water pump 110 communicates the water 100 from the containment reservoir 200 to the water inlet 30 of the water oxygenator 10. A low pressure, high volume air source 120, which may be provided by a turbine or the like, supplies air 90 to the air inlet tube 40 of the water oxygenator 10. After passage through the water oxygenator 10, high oxygen content water is discharged from the outlet 50 in an environmentally compliant condition.
As seen in reference to Table 1, the water oxygenator and oxygenation system is effective in significantly elevating the dissolved oxygen content of the water in the retention reservoir for discharge into a waterway.
Retention Discharge Water
Reservoir Water Dissolved Oxygen
Units Conditions After Treatment
Dissolved Oxygen (ppm) 0.14 7.05
pH 7.1 —
Temperature (° C.) 24.6 —
Dissolved Oxygen (ppm) 0.27 7.31
pH 7.1 —
Temperature (° C.) 24.7 —
Dissolved Oxygen (ppm) 0.31 7.30
pH 7.1
Temperature (° C.) 24.3
The foregoing results were obtained with a water oxygenator 10 having a water inlet 30 of 3 inches, a diameter of 5 inches along the sidewall 60, and a water outlet diameter of 3 inches. The water flow 80 through the water oxygenator was maintained at a nominal flow of 100 gallons per minute. The air flow 90 through the water oxygenator 10 was maintained at a nominal flow of 50 SCFM at a pressure of 4 psi.
It should be understood, of course, that the foregoing relates to exemplary embodiments of the invention and that modifications may be made without departing from the spirit and scope of the invention as set forth in the following claims.

Claims (12)

What is claimed is:
1. A water oxygenator, comprising:
an elongate cylindrical tube having a first end, a second end, an outer sidewall defining a main mixing chamber within an interior cavity of the elongate cylindrical tube;
a plurality of baffles, each comprising a rectangular plate with an arcuate edge surface defined along first opposed ends of the rectangular plate and a generally linear side edge defined along second opposed ends of the plate, the plurality of baffles radially offset and disposed in a spaced apart relation along a longitudinal length of the main mixing chamber;
a water inlet at the first end, the water inlet adapted to be coupled to a source of water contained in a retention reservoir, the water inlet having a diameter less than a diameter of the elongate cylindrical tube;
a water outlet at the second end, having a diameter less than diameter of the elongate cylindrical tube;
a first frusto-conical sidewall connecting the water inlet with the outer sidewall, the frusto-conical sidewall defining an initial mixing chamber; and
an air inlet tube protruding through the first frusto-conical sidewall and oriented in a downstream direction into an initial mixing chamber defined within the frusto-conical sidewall, the air inlet tube adapted to be coupled to a high-volume, low-pressure air source.
2. The water oxygenator of claim 1, wherein each of the plurality of baffles are attached to an interior sidewall of the elongate cylindrical tube at the arcuate edge surface.
3. The water oxygenator of claim 2, wherein each of the plurality of baffles are radially offset 90 degrees from each other along a longitudinal length of the main mixing chamber.
4. The water oxygenator of claim 1, the air inlet tube further comprising:
an injector defined at a distal end of the air inlet tube, the injector oriented to project in a downstream direction along a longitudinal centerline of the initial mixing chamber.
5. The water oxygenator of claim 4, wherein an upstream side of the injector and the air inlet tube are oriented to obstruct a water flow from the source of water to introduce a turbulent zone at an exit of the injector within the initial mixing chamber.
6. The water oxygenator of claim 1, further comprising:
a second frusto-conical sidewall connecting the outer sidewall with the water outlet.
7. A system for oxygenating a source of water held within a containment reservoir, comprising:
a water oxygenator formed as an elongate cylindrical tube having a first end, a second end, an outer sidewall defining a main mixing chamber within an interior cavity, a water inlet at the first end, a fluid outlet at the second end configured to discharge a flow of oxygenated water from the water oxygenator, a plurality of baffles within the interior cavity each comprising a rectangular plate with an arcuate edge surface defined along first opposed ends of the rectangular plate and a generally linear side edge defined along second opposed ends of the plate, the plurality of baffles disposed in a spaced apart radially offset relation along a longitudinal length of the elongate cylindrical tube, a first frusto-conical sidewall connecting the water inlet with the elongate cylindrical tube defining an initial mixing chamber therein, and an air inlet tube projecting through the first frusto-conical sidewall into the initial mixing chamber;
a water pump configured to communicate the source of water from the containment reservoir to the water inlet at a nominal flow rate of 100 gallons per minute, the source of water having a dissolved oxygen concentration of less than 1 parts per million; and
an air source configured to deliver a nominal flow of 50 standard cubic feet per minute at a pressure of 4 psi to the air inlet tube, wherein a dissolved oxygen concentration of the flow of oxygenated water from the water oxygenator is at least 7 parts per million.
8. The system of claim 7, wherein each of the plurality of baffles further comprises:
a rectangular plate;
an arcuate edge surface defined along first opposed ends of the rectangular plate; and
a generally linear side edge defined along second opposed ends of the rectangular plate.
9. The system of claim 8, wherein each of the plurality of baffles are attached to an interior sidewall of the elongate cylindrical tube at the arcuate edge surface.
10. The system of claim 7, the air inlet tube further comprising:
an injector defined at a distal end of the air inlet tube, the injector oriented to project in a downstream direction along a longitudinal centerline of the initial mixing chamber.
11. The system of claim 10, wherein an upstream side of the injector and the air inlet tube are oriented to obstruct a water flow from the source of water to introduce a turbulent zone at an exit of the injector within the initial mixing chamber.
12. The system of claim 7, further comprising:
a second frusto-conical sidewall connecting the outer sidewall with the fluid outlet.
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